在 7 和 16 巴、含水量高达 300 ppm 的二氧化碳液化条件下进行船舶运输的固体形成实验研究

IF 3.8 3区 工程技术 Q2 ENGINEERING, CHEMICAL
Asmira Delic, Xiaoyun Li, Stian Trædal, Knut Maråk, Thor Mejdell, Kai Hjarbo, David Berstad, Hans Georg Jacob Stang
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引用次数: 0

摘要

二氧化碳的船舶运输对于开发碳捕集与封存(CCS)基础设施至关重要。将液态二氧化碳的船舶运输压力从传统的 14-18 巴降低到 7 巴,可提高船舶运输能力,从而显著降低成本。然而,压力的降低需要采取严格的水露点控制措施,以防止形成冰和二氧化碳水合物,从而堵塞管道和设备。二氧化碳完全脱水所需的资金和能源会增加系统的资本支出(CAPEX)和运营支出(OPEX)。因此,了解二氧化碳气流中水含量的限制以及该系统因运行故障而无法达到脱水规范的后果非常重要。本研究通过实验研究了在 16 巴和 7 巴的船舶运输条件下,二氧化碳液化过程中可能形成的固体,其中含有不同浓度的水。使用来自燃烧后胺捕集厂的二氧化碳流来代表真实的二氧化碳成分,在不同的液化压力和含水量下进行了五次测试。实验结果与纯二氧化碳的水合物平衡预测结果进行了比较。结果发现,在含有 200ppm 水的低压二氧化碳液化中,大约 6.7 巴时开始出现固体形成的迹象,当压力进一步降低到 6.5 巴时,过滤器在大约 1 小时内完全堵塞。这明显高于三重点压力,因此形成的固体很可能是水合物。对于含有 100 ppm 水的低压二氧化碳液化,在非常接近三相点和水合物形成区的位置运行时,过滤器上的压降没有增加。在 16 巴的中压二氧化碳液化中,水含量为 200 和 300 ppm 时,没有观察到固体形成的迹象。这些研究结果表明,在用于船舶运输的低压和中压二氧化碳液化过程中,如果水含量超过当前的规定,就会产生影响。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Experimental Investigation of Solid Formation under CO2 Liquefaction Conditions for Ship Transport at 7 and 16 Bar with Water Content up to 300 ppm

Experimental Investigation of Solid Formation under CO2 Liquefaction Conditions for Ship Transport at 7 and 16 Bar with Water Content up to 300 ppm
Ship-based transport of CO2 is crucial in developing a carbon capture and storage (CCS) infrastructure. Lowering the ship transport pressure of liquid CO2 from the conventional 14–18 to 7 bar increases the vessel-based transport capacity, leading to significant cost reductions. However, this reduction in pressure necessitates stringent water dew point control measures to prevent the formation of ice and CO2 hydrates, which could block pipelines and equipment. The capital and energy demands of complete dehydration of CO2 increase the CAPEX and the OPEX of the system. It is therefore important to know the limits for water content in the CO2 stream and the consequences if this system cannot reach the dehydration specification due to operational upsets. This study experimentally investigated possible solid formation under CO2 liquefaction for ship transport conditions at 16 and 7 bar, containing varying water concentrations. Using a CO2 stream from a postcombustion amine-based capture plant to represent a realistic CO2 composition, five tests were conducted at different liquefaction pressures and water contents. The experimental results were compared to the hydrate equilibrium predictions for pure CO2. It was found that, for low-pressure CO2 liquefaction with 200 ppm water, signs of solid formation started to occur at about 6.7 bar, which led to complete blocking of the filter over the course of approximately 1 h as the pressure was further reduced to 6.5 bar. This is clearly above the triple point pressure, so the solids that formed were most likely hydrates. For low-pressure CO2 liquefaction with 100 ppm of water operating very close to the triple point and the hydrate formation area, there was no increase in the pressure drop across the filter. For medium-pressure CO2 liquefaction at 16 bar, no indication of solid formation was observed with a water content of 200 and 300 ppm. These findings show the effects of exceeding the current water specification during liquefaction of low- and medium-pressure CO2 for ship transport.
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来源期刊
Industrial & Engineering Chemistry Research
Industrial & Engineering Chemistry Research 工程技术-工程:化工
CiteScore
7.40
自引率
7.10%
发文量
1467
审稿时长
2.8 months
期刊介绍: ndustrial & Engineering Chemistry, with variations in title and format, has been published since 1909 by the American Chemical Society. Industrial & Engineering Chemistry Research is a weekly publication that reports industrial and academic research in the broad fields of applied chemistry and chemical engineering with special focus on fundamentals, processes, and products.
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